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<br />Facility Process Comoonent <br />Disinfection/Outfall <br /> <br />$12,760,000 <br />Total Cost <br /> <br />Costs <br /> <br />Design/Construction <br /> <br />FUNDING SOURCE <br />Capital Reserve <br /> <br />PROJECT: <br /> <br />DESCRIPTION: <br /> <br />JUSTIFICATION: <br /> <br />PROJECT DRIVER: <br />PROJECT TRIGGER: <br />TYPE OF PROJECT: <br /> <br />ESTIMATED PROJECT COST <br />(FY 2004-05 Dollars): <br /> <br />RECOSTED PROJECT COST <br />(FY 2007-08 Dollars): <br /> <br />PHASING: <br /> <br />4f A ~ .., <br /> <br />SODIUM HYPOCHLORITE CONVERSION <br /> <br />TOTAL <br /> <br /> <br />TOTAL <br /> <br />Sodium Hypochlorite Conversion <br /> <br />Convert existing chlorine gas system to sodium hypochlorite for the base flow. Retain the <br />existing chlorine contact basins. Install system with capability for high rate disinfection of <br />PE diversion assuming high dosages of chlorine into a 72-inch pipe and small chlorine <br />contact basin. <br /> <br />Liquid sodium hypochlorite and sodium bisulfite system will replace the existing chlorine <br />sulfur dioxide gas systems and increase the disinfection capacity from 175 mgd to 277 <br />mgd. <br /> <br />Operator and community safety issues. <br /> <br />Phasing with other related projects. <br />50% Capacity; 50% Performance <br /> <br />$4,100,000 <br /> <br />$12,760,000 <br /> <br />Programmed for FY 2007/08 <br /> <br />Page 75 <br /> <br />FY 06-07 BUDGET AND CIP <br />